Method and apparatus for reducing decomposition byproducts in a methanol to olefin reactor system
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
C07C-001/20
C07C-001/00
출원번호
US-0175285
(2002-06-19)
발명자
/ 주소
Clem,Kenneth Ray
Vaughn,Stephen N.
Xu,Teng
White,Jeffrey L.
출원인 / 주소
ExxonMobil Chemical Patents Inc.
인용정보
피인용 횟수 :
1인용 특허 :
18
초록▼
Disclosed is a method and apparatus for reducing the amount of metal catalyzed side-reaction byproducts formed in the feed vaporization and introduction system of a methanol to olefin reactor system by monitoring and/or maintaining the temperature of at least a portion of the feed vaporization and i
Disclosed is a method and apparatus for reducing the amount of metal catalyzed side-reaction byproducts formed in the feed vaporization and introduction system of a methanol to olefin reactor system by monitoring and/or maintaining the temperature of at least a portion of the feed vaporization and introduction system and/or of the feedstock contained therein below about 400째 C., 350째 C., 300째 C., 250째 C. , 200째 C. or below about 150째 C. The temperature can be maintained in the desired range by jacketing at least a portion of the feed vaporization and introduction system, such as at least a portion of the feed introduction nozzle, with a thermally insulating material or by implementing a cooling system.
대표청구항▼
What is claimed is: 1. A method for making an olefin product from a feedstock comprising an alcohol and/or an ether, comprising: directing the feedstock through a feed introduction nozzle having an inner surface and being attached to a reactor, wherein at least a portion of the nozzle is jacketed w
What is claimed is: 1. A method for making an olefin product from a feedstock comprising an alcohol and/or an ether, comprising: directing the feedstock through a feed introduction nozzle having an inner surface and being attached to a reactor, wherein at least a portion of the nozzle is jacketed with a thermally insulating material; maintaining the inner surface of the nozzle at a temperature below 350째 C; and contacting, in the reactor, the feedstock with a molecular sieve catalyst at a temperature of from 350째 C. to 600째 C. to form an effluent comprising light olefins. 2. The method of claim 1, wherein the inner surface of the nozzle is maintained at a temperature below 300째 C. 3. The method of claim 2, wherein the inner surface of the nozzle is maintained at a temperature below 250째 C. 4. The method of claim 3, wherein the inner surface of the nozzle is maintained at a temperature below 200째 C. 5. The method of claim 4, wherein the inner surface of the nozzle is maintained at a temperature below 150째 C. 6. The method of claim 1, wherein the material is selected from the group consisting of fire brick, alumina bricks, silica bricks, magnesite bricks, chrome bricks, silicon carbide bricks, zircon, zirconia, forsterite, high temperature calcium silicate, alumina and silica-alumina ceramics, diatomaceous silica, cements, fillers, calcium carbonate, calcium sulfate, concrete, glass, granite, marble, mineral wool, porcelain, portland cement, Pumice stone, and gunnite. 7. The method of claim 6, wherein the thermally insulating material covers at least a portion of the exterior portion of the nozzle extending outside the reactor. 8. The method of claim 1, wherein the thermally insulating material covers at least a portion of an interior portion of the nozzle extending inside the reactor. 9. The method of claim 1, further comprising: cooling at least a portion of the inner surface of the nozzle with a cooling system. 10. A method for making an olefin product from an oxygenate-containing feedstock, comprising: directing the feedstock through a feed nozzle having a nozzle temperature below 350째 C. and being attached to a reactor, wherein at least a portion of the nozzle is covered by a thermally insulating material; and contacting, in the reactor, the feedstock with a catalyst at a temperature of from 350째 C. to 600째 C. to form an effluent comprising light olefins. 11. The method of claim 10, wherein the material is selected from the group consisting of fire brick, alumina bricks, silica bricks, magnesite bricks, chrome bricks, silicon carbide bricks, zircon, zirconia, forsterite, high temperature calcium silicate, alumina and silica-alumina ceramics, diatomaceous silica, cements, fillers, calcium carbonate, calcium sulfate, concrete, glass, granite, marble, mineral wool, porcelain, portland cement, Pumice stone, and gunnite. 12. The method of claim 11, wherein the thermally insulating material coven at least a portion of an interior portion of the nozzle extending inside the reactor. 13. The method of claim 12, wherein the thermally insulating material covers at least a portion of the exterior portion of the nozzle extending outside the reactor. 14. A method for making an olefin product from an oxygenate-containing feedstock, comprising: heating the feedstock in a heating device to form a heated feedstock; directing the heated feedstock through a feed nozzle attached to a reactor, cooling at least a portion of the nozzle with a cooling system to a temperature below 350째 C.; and contacting, in the reactor, the feedstock with a catalyst at a temperature of from 350째 C. to 600째 C. to form an effluent comprising light olefins. 15. The method of claim 14, wherein a cooling medium cools the nozzle, the method further comprising: directing the cooling medium into the reactor wherein the cooling medium mixes with the feedstock. 16. A method for making an olefin product from a feedstock comprising an alcohol and/or an ether, comprising: directing the feedstock through a feed introduction nozzle having an inner surface and being attached to a reactor, wherein at least a portion of the nozzle is insulated with a thermally insulating material; maintaining the feedstock below 350째 C. while the feedstock is in the nozzle; and contacting, in the reactor, the feedstock with a molecular sieve catalyst at a temperature of from 350째 C. to 600째 C. to form an effluent comprising light olefins. 17. The method of claim 16, wherein the feedstock is maintained below 300째 C. while the feedstock is in the nozzle. 18. The method of claim 17, wherein the feedstock is maintained below 250째 C. while the feedstock is in the nozzle. 19. The method of claim 18, wherein the feedstock is maintained below 200째 C. while the feedstock is in the nozzle. 20. The method of claim 19, wherein the feedstock is maintained below 150째 C. while the feedstock is in the nozzle. 21. The method of claim 16, further comprising: cooling at least a portion of the nozzle with a cooling medium. 22. The method of claim 21, further comprising: insulating at least a portion of the nozzle with a thermally insulating material.
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